[go: up one dir, main page]

WO2012144277A1 - Scale inhibition method and geothermal power generating device - Google Patents

Scale inhibition method and geothermal power generating device Download PDF

Info

Publication number
WO2012144277A1
WO2012144277A1 PCT/JP2012/055545 JP2012055545W WO2012144277A1 WO 2012144277 A1 WO2012144277 A1 WO 2012144277A1 JP 2012055545 W JP2012055545 W JP 2012055545W WO 2012144277 A1 WO2012144277 A1 WO 2012144277A1
Authority
WO
WIPO (PCT)
Prior art keywords
geothermal water
concentration
geothermal
water
inorganic cation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2012/055545
Other languages
French (fr)
Japanese (ja)
Inventor
邦幸 高橋
義隆 川原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to US14/009,296 priority Critical patent/US9840429B2/en
Priority to PH1/2013/502042A priority patent/PH12013502042B1/en
Priority to NZ615602A priority patent/NZ615602B2/en
Priority to JP2013510917A priority patent/JP5839030B2/en
Publication of WO2012144277A1 publication Critical patent/WO2012144277A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/528—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
    • E—FIXED CONSTRUCTIONS
    • E21—EARTH OR ROCK DRILLING; MINING
    • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B37/00—Methods or apparatus for cleaning boreholes or wells
    • E21B37/06—Methods or apparatus for cleaning boreholes or wells using chemical means for preventing or limiting, e.g. eliminating, the deposition of paraffins or like substances
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G4/00—Devices for producing mechanical power from geothermal energy
    • F03G4/074—Safety arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G7/00—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for
    • F03G7/04—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for using pressure differences or thermal differences occurring in nature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24T—GEOTHERMAL COLLECTORS; GEOTHERMAL SYSTEMS
    • F24T10/00—Geothermal collectors
    • F24T10/30—Geothermal collectors using underground reservoirs for accumulating working fluids or intermediate fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/001—Upstream control, i.e. monitoring for predictive control
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/005—Processes using a programmable logic controller [PLC]
    • C02F2209/006—Processes using a programmable logic controller [PLC] comprising a software program or a logic diagram
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/02—Temperature
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/40—Liquid flow rate
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/10—Energy recovery
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/22—Eliminating or preventing deposits, scale removal, scale prevention
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/083—Mineral agents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • C02F5/12—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing nitrogen
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • C02F5/14—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing phosphorus
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/10—Geothermal energy
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/30—Wastewater or sewage treatment systems using renewable energies

Definitions

  • the present invention relates to a method for suppressing a scale containing inorganic cations such as calcium, and a geothermal power generation apparatus that generates electricity using geothermal water while suppressing the precipitation of these scales.
  • Geothermal power generation is a method in which high-temperature geothermal water is collected from production wells and is generated using steam separated from the geothermal water. The geothermal water from which the steam has been separated is returned to the ground from the reduction well.
  • geothermal water collected from production wells contains more inorganic ions such as calcium and dissolved silica than well water and river water.
  • the geothermal water collected from the production well is high temperature, but the inorganic cation and dissolved silica are concentrated and the temperature of the geothermal water is lowered by the flash process of extracting steam from the geothermal water by decompression. Moreover, it is gradually cooled as it circulates in the piping in the power plant, and the solubility of inorganic cations and dissolved silica decreases.
  • the silica contained in the geothermal water becomes supersaturated, it is polymerized to become amorphous silica, which precipitates as silica scale.
  • the inorganic cation forms a salt such as carbonate and precipitates. These scales may adhere to the pipe inner wall of the power generator and cause a pipe blockage or the like.
  • Patent Document 1 it has been conventionally practiced to add acid to geothermal water to lower the pH to suppress silica scale precipitation.
  • the lower the pH the lower the polymerization rate of the silica.
  • the silica polymerization rate decreases and the silica scale does not easily precipitate in the piping of the geothermal power generation device. is there.
  • Patent Document 2 a chemical solution is injected into a production well to suppress precipitation of inorganic cation salts such as calcium carbonate, anhydrite, and magnesium silicate in the production well. ing.
  • the solubility of amorphous silica increases as it becomes alkaline, and is said to increase rapidly especially at pH 8 or higher. Therefore, precipitation of silica scale can be suppressed by increasing the pH of the geothermal water.
  • silica and inorganic cations sometimes form salts and precipitate as scales.
  • a salt of silica and an inorganic cation is obtained by injecting a scale-preventing agent into a production well and removing inorganic ions contained in geothermal water.
  • geothermal water contains a large amount of inorganic cations, so if you try to remove all inorganic cations in the geothermal water, the treatment costs will increase and the economics of the geothermal power plant will increase. Operation was difficult.
  • an object of the present invention is to provide a method for suppressing a scale containing an inorganic cation such as calcium, and a geothermal power generation apparatus that can be economically operated while suppressing the precipitation of these scales.
  • the scale suppression method of the present invention comprises: An influent measurement process for measuring the flow rate of geothermal water collected from the production well and the concentration of inorganic cations of 2 or more, A heat removal step of removing heat of the geothermal water; An effluent measurement step for measuring the temperature and pH of the geothermal water after the heat removal step; Based on the temperature and pH of the geothermal water after the heat removal step, the inorganic cation saturation concentration of the geothermal water after the heat removal step is obtained, and the inorganic of the geothermal water measured in the influent measurement step Necessary for suppressing precipitation of salt containing inorganic cation from the value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the heat removal step from the cation concentration and the flow rate of the geothermal water.
  • the scale control method of the present invention first, the flow rate of geothermal water collected from a production well and the concentration of divalent or higher inorganic cations are measured, and the temperature and pH of the geothermal water after the heat removal step are measured. measure. Then, based on the temperature and pH of the geothermal water after the heat removal step, the saturation concentration of the inorganic cation of the geothermal water after the heat removal step is obtained, and the inorganic cation of the preheated water measured in the influent measurement step Calculate the amount of scale inhibitor added to suppress the precipitation of salts containing inorganic cations from the concentration minus the saturation concentration of the inorganic cation after the heat removal step and the flow rate of the geothermal water. To do.
  • the scale inhibitor is added to the geothermal water collected from the production well.
  • the geothermal water after the heat removal step it is possible to add a scale inhibitor according to the amount of the inorganic cation that is deposited at a saturation concentration or higher, and it is possible to suppress the precipitation of scale, and the amount of the scale inhibitor added Can be minimized.
  • each of the sample waters is prepared by increasing the inorganic cation concentration little by little at the same silica concentration and pH as the geothermal water collected from the production well. After holding the temperature after the heat removal step for a predetermined time, when measuring the inorganic cation concentration in each treated water, when the inorganic cation concentration of the treated water first becomes lower than the inorganic cation concentration of the sample water It is preferable that the concentration of the sample water is the saturation concentration.
  • the inorganic cation concentration of the sample water when the inorganic cation concentration of the treated water first becomes lower than the inorganic cation concentration of the sample water, precipitation of the salt containing the inorganic cation is obtained.
  • the saturation concentration at which can begin can be determined.
  • the silica concentration, pH, temperature after heat treatment removal varies, by obtaining the saturation concentration in advance under various conditions in which the silica concentration, pH, temperature after the heat removal step is changed, Based on the temperature and pH of the geothermal water after the heat removal step, the saturation concentration of the inorganic cation of the geothermal water after the heat removal step can be determined.
  • the inorganic cation is preferably at least one selected from magnesium ion, calcium ion, divalent iron ion, trivalent iron ion and aluminum ion. Any of the above inorganic cations reacts with silica under alkaline conditions to form a salt that is difficult to dissolve and is likely to precipitate, so that it is highly necessary to apply the method of the present invention.
  • the scale suppression method of the present invention it is preferable to adjust the pH of the geothermal water to 9 or more.
  • the pH of the geothermal water By setting the pH of the geothermal water to 9 or more, it is possible to increase the solubility of silica and suppress the generation of scale.
  • the scale suppression method of the present invention it is preferable to adjust the pH to 9 or more by adding an alkaline agent to the geothermal water simultaneously with the addition of the scale inhibitor or after the addition of the scale inhibitor. Simultaneously with the addition of the scale inhibitor to the geothermal water, or after the addition of the scale inhibitor, the alkaline agent is added to adjust the pH to 9 or more, thereby preventing salt precipitation due to inorganic cations in the addition of the alkaline agent. can do.
  • the heat removal step of the scale suppression method of the present invention preferably includes a step of reducing the pressure of the geothermal water and taking out water vapor and / or a step of recovering heat from the geothermal water and evaporating the power generation medium.
  • power generation can be performed using the heat of geothermal water.
  • the scale suppression method of the present invention gas-liquid separates geothermal water collected from the production well, supplies steam after gas-liquid separation to a power generation facility, and uses the geothermal water after gas-liquid separation in the heat removal step. It is preferable to send. According to this aspect, heat can be further recovered from the geothermal water after separating the steam to generate power.
  • the geothermal power generator of the present invention is An inorganic cation concentration measuring device that measures the concentration of divalent or higher inorganic cations in geothermal water collected from production wells; A flow meter for measuring the flow rate of geothermal water collected from the production well; A heat removal section for lowering the temperature of the geothermal water; A thermometer for measuring the temperature of the geothermal water after the heat removal; A pH measuring device for measuring the pH of the geothermal water after the heat removal; Based on the temperature and pH of the geothermal water after the temperature is lowered at the heat removal unit, the saturation concentration of the inorganic cation of the geothermal water after the temperature is lowered at the heat removal unit is determined, and the inorganic A value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the temperature has been lowered by the heat removal unit from the inorganic cation concentration of the geothermal water measured by a cation concentration measuring device, and the geothermal water From the flow rate of
  • the geothermal power generation device of the present invention in the arithmetic processing unit, the geothermal heat after the temperature is reduced by the heat removal unit based on the temperature measured by the thermometer and the pH measured by the pH measurement device. Obtain the saturated concentration of inorganic cations in water. Next, from the value obtained by subtracting the saturation concentration from the inorganic cation concentration measured by the inorganic cation concentration measuring device and the flow rate measured by the flow meter, the amount of inorganic cation that is expected to precipitate as it is calculated. The amount of the scale inhibitor added to suppress the precipitation of that amount of inorganic cation is calculated. In the control unit, by adding the amount of the scale inhibitor calculated by the arithmetic processing unit, the amount of the scale inhibitor added can be minimized while suppressing the precipitation of scale.
  • the geothermal power generation apparatus of the present invention is preferably configured so that a gas-liquid separator is disposed in front of the heat removal unit, and geothermal water after gas-liquid separation is introduced into the heat removal unit. According to this aspect, heat recovery can be further performed using the geothermal water after collecting steam for power generation from the geothermal water.
  • the heat removal unit of the geothermal power generation apparatus of the present invention is one or more types selected from a heat radiating pipe, a flasher that extracts steam from geothermal water by decompression, and a heat exchanger that heats the power generation medium to evaporate the power generation medium.
  • a heat radiating pipe Preferably there is.
  • the geothermal power generation apparatus of the present invention includes a solution storage unit that stores sample water, a temperature control unit that adjusts the temperature of the sample water stored in the solution storage unit, and an acid in the sample water stored in the solution storage unit.
  • a pH adjusting unit for adjusting pH by adding alkali a concentration measuring unit for measuring a divalent or higher valent inorganic cation concentration in a sample water after a predetermined time, and gradually adjusting the inorganic cation concentration as sample water
  • a saturation concentration measuring device for an inorganic cation having a solution supply unit that creates an enhanced one and sequentially flows into the solution storage unit.
  • the saturation concentration of inorganic cations under various pH and temperature conditions can be measured in advance by changing the pH and temperature of the sample water, the temperature and pH of the geothermal water can be measured.
  • the saturation concentration of the inorganic cation in the geothermal water can be obtained.
  • the scale inhibitor is added to the geothermal water collected from the production well. Therefore, in the geothermal water after the heat removal step, it is possible to add a scale inhibitor according to the amount of the inorganic cation deposited at a saturation concentration or more, and suppress the precipitation of the scale, and the addition amount of the scale inhibitor Can be minimized.
  • the arithmetic processing unit calculates the amount of inorganic cations that are predicted to precipitate as they are, and the scale inhibitor necessary for suppressing the precipitation of the inorganic cations of that amount.
  • the amount of the scale inhibitor added is minimized while suppressing the precipitation of scale. The power generator can be operated economically.
  • geothermal water collected from the production well 10 is sent to the separator 11 through the pipe L1.
  • hot water and steam are separated, and the steam is sent to the first turbine 12 via the pipe L ⁇ b> 3, and power is generated by the first generator 13.
  • the separator 11 has a function of a flasher for extracting steam by depressurizing hot water.
  • the steam that has passed through the first turbine 12 is sent to the condenser 14 via the pipe L4 to become condensed water, further sent to the cooling tower 15 via the pipe L5, cooled, and reduced through a path (not shown). Returned to the well 16.
  • a part of the water cooled by the cooling tower 15 is returned to the condenser 14 via the pipe L6 and used as cooling water for the steam sent from the first turbine 12.
  • the heat is further recovered from the geothermal water separated from the steam by the separator 11, and the inorganic cation reacts with the silica and precipitates as a scale while the recovered geothermal water is returned to the reduction well 16. I try to prevent it. That is, in this embodiment, the geothermal water separated from the steam by the separator 11 corresponds to the geothermal water collected from the production well in the present invention. However, in the present invention, the geothermal water collected from the production well 10 may be used as it is for the medium evaporator 17 described below.
  • the geothermal power generation apparatus equipped with this medium evaporator performs binary power generation using the heat of the geothermal water separated by the separator 11. That is, the geothermal water separated by the separator 11 is sent to the medium evaporator 17 via the pipe L7, where heat exchange is performed to evaporate the low boiling point heat medium, and then the reduction well is connected via the pipe L8. 16 is returned.
  • the medium evaporator 17 corresponds to the heat removal unit in the present invention.
  • the heat medium vaporized by the medium evaporator 17 is sent to the second turbine 18 through the pipe L9, and the second generator 19 generates power. Furthermore, the heat medium that has passed through the second turbine 18 is sent to the medium condenser 20 via the pipe L10, where it becomes a condensate, and further passes through the pipe L11 having the pump 21 in the middle, to the medium evaporator. 17 is returned.
  • a low-boiling-point heat medium that can be vaporized using the heat of the geothermal water separated by the separator 11 is used, and is not particularly limited.
  • normal heptane, isoheptane , Normal pentane, isopentane, normal butane, isobutane, hydrofluoroether, R245fa, R134a, R22, R407c, and the like are preferably used.
  • the geothermal water separated by the separator 11 is recovered by heat through the medium evaporator 17 and then returned to the reduction well 16.
  • the scale was generated and the piping was blocked.
  • a scale inhibitor is added in accordance with the concentration of the divalent or higher valent inorganic cation contained in the geothermal water to suppress the generation of scale due to the salt of the inorganic cation and silica. .
  • the divalent or higher valent inorganic cation is not particularly limited.
  • it is a kind selected from magnesium ion, calcium ion, divalent iron ion, trivalent iron ion and aluminum ion.
  • the scale inhibitor include EDTA, NTA (nitrilotriacetic acid), HIDS (3-hydroxy-2-2′-iminodisuccinic acid), carboxymethylethyleneimine, citric acid, tartaric acid, and various sodium salts thereof.
  • Chelating agents such as potassium salts, ammonium salts and hydrates, PAS (polyacrylic acid Na) and the like.
  • An apparatus configuration for carrying out the above-described scale suppression method will be described with reference to FIG. 1.
  • An inorganic cation concentration meter 22 and a silica concentration meter 23 are provided in a pipe L 7 extending from the separator 11 to the medium evaporator 17. It is connected. Further, the alkaline agent in the alkaline agent tank 24 flows into the downstream of the silica concentration meter via the pump 25, and the chelating agent in the chelating agent tank 26 is connected to the pump 27 at almost the same location. It comes to flow in through.
  • the inflow site of the alkaline agent is preferably the same as the inflow site of the chelating agent or downstream of the inflow site of the chelating agent.
  • the addition amount of the alkaline agent supplied from the alkaline agent tank 24 is adjusted so that the pH of the geothermal water is preferably 9 or more, more preferably 9.5 to 10.0.
  • the addition amount of the chelating agent is adjusted by receiving the signal from the arithmetic processing unit 28 and controlling the pump 27 by the chelating agent addition amount control unit 29.
  • a flow meter 30 is connected further downstream of the inflow point of the alkaline agent in the pipe L7 so that the flow rate of the geothermal water flowing into the medium evaporator 17 can be measured.
  • the installation location of the flow meter 30 is not limited to the above location, and may be upstream of the location where the alkali agent or chelating agent is added.
  • thermometer 31 and a pH meter 32 are connected to the pipe L8 connecting the medium evaporator 17 and the reduction well 16, and the temperature and pH of the geothermal water returned to the reduction well through the medium evaporator 17 are measured. It is supposed to be.
  • the inorganic cation concentration meter 22, the silica concentration meter 23, the flow meter 30, the thermometer 31, and the pH meter 32 are each connected to the arithmetic processing unit 28.
  • a storage device 33 is connected to the arithmetic processing unit 28, and an input device 34 is connected to the storage device 33.
  • FIG. 2 shows an example of an inorganic cation saturation concentration measuring apparatus suitably used in the present invention.
  • the inorganic cation saturation concentration measuring device 40 includes a solution storage unit 41.
  • the solution storage unit 41 includes a temperature control unit 42, a solution collection unit 43, a pH adjustment unit 44, and a cation concentration measurement unit. 45 is connected.
  • the pH adjusting unit 44 is provided with a pH measuring unit 44a and an acid / alkali adding unit 44b.
  • a timer 45 a is attached to the cation concentration measuring unit 45.
  • FIG. 3 shows a flowchart for measuring the saturation concentration of the inorganic cation using the saturation concentration measuring device 40.
  • calcium ion is selected as the inorganic cation, and the precipitation start point (saturation concentration) of calcium silicate is obtained.
  • a reaction solution in which the silica concentration is 600 mg / L and the calcium concentration is gradually increased in the range of 0 to 50 mg / L is prepared, and the solution storage unit 41 is filled through the solution collecting unit 43 (step S1). ).
  • step S2 while measuring the pH by the pH measuring unit 44a of the pH adjusting unit 44, for example, hydrochloric acid or a sodium hydroxide aqueous solution is added from the acid-alkali adding unit 44b, and a predetermined pH, for example, pH 9, 10, 11 It adjusts so that it may become (step S2).
  • a predetermined pH for example, pH 9, 10, 11 It adjusts so that it may become (step S2).
  • reaction liquid adjusted to a predetermined calcium concentration and pH is kept at a constant temperature under predetermined conditions, in this embodiment, 100 ° C. for 3 hours (step S3).
  • This condition is preferably set to be the same as the temperature and time when returning to the reduction well 16 through the medium evaporator 17.
  • the cation concentration measurement unit 45 measures the cation concentration (calcium concentration in this embodiment) (step S4).
  • the calcium concentration can be measured by, for example, EDTA titration or a calcium ion meter.
  • step S5 it is determined whether or not the initially added calcium ion concentration is higher than the calcium ion concentration after the reaction. If NO, the process returns to step S1. In the case of YES, the calcium ion concentration of the sample water at that time (concentration in step S1) is determined as the deposition start point (saturated concentration in the present invention) (step S6), and the process is terminated.
  • a similar measurement may be performed by adjusting a reaction solution in which the concentration of magnesium is gradually increased in step S1.
  • FIG. 4 shows the result of measuring the saturation concentration of calcium at pH 9 by the above method, where the horizontal axis indicates the amount of calcium added (mg / L) during reaction liquid adjustment, and the vertical axis indicates ,
  • the calcium ion concentration after reaction (mg / L, black square graph), and the value obtained by subtracting the calcium ion concentration after reaction from the same calcium addition amount (mg / L, black triangle graph) are shown. Therefore, when the silica concentration is 600 mg / L, and the treatment is performed at 100 ° C. for 3 hours at pH 9, the value obtained by subtracting the calcium ion concentration after reaction from the calcium addition amount is a positive value. 5 mg / L, which is the amount of calcium added to turn to 1.
  • FIG. 5 shows the results of measuring the saturation concentration of calcium at each pH by repeating the measurement shown in FIG. 3 under various pH conditions. Thus, it turns out that the saturation concentration of calcium falls as pH rises.
  • the pH is changed with respect to the saturation concentration of each inorganic cation when processing is performed under predetermined conditions set to be similar to the temperature and time when returning to the reduction well 16 through the medium evaporator 17.
  • the data measured in advance is obtained in advance, and the data is input from the input device 34 of FIG. 1 to the storage device 33 and stored. When the temperature and time fluctuate, the data is obtained under various conditions.
  • the calculation processing unit 28 in FIG. 1 calculates the addition amount of the chelating agent that is a scale inhibitor, and controls the pump 27 by the chelating agent addition amount control unit 29 to add a predetermined amount of the chelating agent. This will be described with reference to FIG.
  • the above measurement is performed from the data of the saturated concentration of each inorganic cation stored in the storage device 33 under various conditions.
  • the saturation concentration of the inorganic cation in the geothermal water under the determined conditions is determined (step S1).
  • step S12 a value obtained by subtracting the saturation concentration determined above from the inorganic cation concentration of the geothermal water measured by the inorganic cation concentration meter 22 is calculated (step S12).
  • the concentration of the inorganic cation in the geothermal water increases, so the concentration rate is estimated from the amount of evaporation to obtain the inorganic cation concentration of the geothermal water.
  • step S13 prediction is made when a scale inhibitor (chelating agent) is not added from the flow rate of the geothermal water measured by the flow meter 30 and the value obtained by subtracting the saturation concentration from the inorganic cation concentration of the geothermal water.
  • the amount of inorganic cations deposited as scale is calculated (step S13).
  • step S14 the addition amount of a scale inhibitor (chelating agent) necessary for suppressing the precipitation of the inorganic cation having the predicted precipitation amount is calculated (step S14).
  • the operation of FIG. 6 by the arithmetic processing unit 28 is performed, for example, every predetermined time so that an appropriate amount of precipitation inhibitor is always added to the geothermal water.
  • the first turbine 12 while preventing the geothermal water from depositing scale in the pipe, the first turbine 12 generates power with the first generator 13 and the second turbine 18 generates power with the second generator 19.
  • the first turbine 12 generates power with the first generator 13 and the second turbine 18 generates power with the second generator 19.
  • the addition amount of the scale precipitation inhibitor (chelating agent) can be suppressed to the minimum necessary, economical operation becomes possible.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Sustainable Energy (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Fluid Mechanics (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Thermal Sciences (AREA)
  • Sustainable Development (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

Provided are a method for inhibiting scale including inorganic cations such as, for example, calcium and a geothermal power generating device that can be economically operated while inhibiting the deposition of the scale. The geothermal power generating device comprises: an inorganic cation concentration measuring device (22) for measuring the concentration of bivalent or more inorganic cations in geothermal water collected from a production well (10); a flowmeter (30) for measuring the flow rate of the geothermal water collected from the production well; a heat removal unit (17) for lowering the temperature of the geothermal water; a thermometer (31) for measuring the temperature of the geothermal water after removing heat; a pH measuring device (32) for measuring the pH of the geothermal water after removing heat; a calculation processing unit (28) for calculating the additive amount of a scale inhibitor, according to the value obtained by subtracting the saturation concentration of inorganic cations in the geothermal water after removing heat from the measured value by the inorganic cation concentration measuring device (22), the measured value by the flowmeter (30), the measured value by the thermometer (31), and the measured value by the pH measuring device (32); and a control unit (29) for adding the scale inhibitor to the geothermal water by the amount calculated by the calculation processing unit (28).

Description

スケール抑制方法及び地熱発電装置Scale suppression method and geothermal power generator

　本発明は、カルシウムなどの無機陽イオンを含むスケールの抑制方法及び、これらのスケールの析出を抑制して地熱水を用いて発電を行う地熱発電装置に関する。 The present invention relates to a method for suppressing a scale containing inorganic cations such as calcium, and a geothermal power generation apparatus that generates electricity using geothermal water while suppressing the precipitation of these scales.

　地熱発電は、生産井から高温の地熱水を採取し、地熱水から分離した蒸気を利用して発電を行うものである。蒸気を分離した地熱水は、還元井から地中に返還される。 Geothermal power generation is a method in which high-temperature geothermal water is collected from production wells and is generated using steam separated from the geothermal water. The geothermal water from which the steam has been separated is returned to the ground from the reduction well.

　ところで、生産井から採取される地熱水は、井戸水や河川水よりもカルシウム等の無機イオンや、溶存シリカを多く含んでいる。 By the way, geothermal water collected from production wells contains more inorganic ions such as calcium and dissolved silica than well water and river water.

　生産井から採取した地熱水は高温であるが、減圧により地熱水から蒸気を取出すフラッシュ工程により、無機陽イオンや溶存シリカが濃縮されるとともに、地熱水の温度が低下する。また発電所内の配管内を流通するうちに徐々に冷やされていき、無機陽イオンや溶存シリカの溶解度が低下する。地熱水に含まれるシリカが過飽和状態となると、重合して非晶質シリカとなり、シリカスケールとして析出する。また、無機陽イオンは、炭酸塩等の塩を形成して析出する。これらのスケールは、発電装置の配管内壁などに付着して、配管閉塞等を生じる恐れがある。 The geothermal water collected from the production well is high temperature, but the inorganic cation and dissolved silica are concentrated and the temperature of the geothermal water is lowered by the flash process of extracting steam from the geothermal water by decompression. Moreover, it is gradually cooled as it circulates in the piping in the power plant, and the solubility of inorganic cations and dissolved silica decreases. When the silica contained in the geothermal water becomes supersaturated, it is polymerized to become amorphous silica, which precipitates as silica scale. In addition, the inorganic cation forms a salt such as carbonate and precipitates. These scales may adhere to the pipe inner wall of the power generator and cause a pipe blockage or the like.

　例えば特許文献１に記載されるように、地熱水に酸を加えてｐＨを低下させて、シリカスケールの析出を抑制することが従来より行われている。シリカの重合速度は、ｐＨが低いほど遅くなるので、地熱水のｐＨを低下させることで、シリカの重合速度が低下し、地熱発電装置の配管内でシリカスケールが析出しにくくなるというものである。 For example, as described in Patent Document 1, it has been conventionally practiced to add acid to geothermal water to lower the pH to suppress silica scale precipitation. The lower the pH, the lower the polymerization rate of the silica. By lowering the pH of the geothermal water, the silica polymerization rate decreases and the silica scale does not easily precipitate in the piping of the geothermal power generation device. is there.

　また、特許文献２に記載されるように、生産井に薬液を注入し、生産井内における炭酸カルシウム、硬石膏、マグネシウム珪酸塩等の無機陽イオンの塩の析出を抑制することが従来より行われている。 Moreover, as described in Patent Document 2, a chemical solution is injected into a production well to suppress precipitation of inorganic cation salts such as calcium carbonate, anhydrite, and magnesium silicate in the production well. ing.

特開平６－３０４５９５号公報JP-A-6-304595 特開平５－１９５６８４号公報JP-A-5-195684

　地熱水のｐＨを低下させても、シリカの重合速度を低下させるだけなので、地熱水を還元井に返還するに際し、時間を要する場合においては、シリカスケールの析出を十分に抑制できるとは限らなかった。また、酸によって配管等が腐食するおそれがあった。更には、酸として硫酸を使用した場合においては、硬石膏等のスケールが析出するおそれがあった。 Even if the pH of geothermal water is lowered, it only reduces the polymerization rate of silica, so when it takes time to return the geothermal water to the reduction well, it is possible to sufficiently suppress the precipitation of silica scale. It was not limited. Moreover, there was a possibility that piping etc. might corrode with acid. Furthermore, when sulfuric acid is used as the acid, scales such as anhydrite may be deposited.

　一方、非晶質シリカの溶解度は、アルカリ性になるほど高くなり、特にｐＨ８以上で急激に上昇するとされている。そのため、地熱水のｐＨを高めることでシリカスケールの析出を抑制できる。 On the other hand, the solubility of amorphous silica increases as it becomes alkaline, and is said to increase rapidly especially at pH 8 or higher. Therefore, precipitation of silica scale can be suppressed by increasing the pH of the geothermal water.

　しかしながら、地熱水のｐＨをアルカリ性にするに伴い、シリカと無機陽イオンとが塩を形成してスケールとして析出することがあった。 However, as the pH of geothermal water is made alkaline, silica and inorganic cations sometimes form salts and precipitate as scales.

　これに対して、特許文献２に記載されるように、生産井にスケール防止用の薬剤を注入して、地熱水に含まれる無機イオンを除去することで、シリカと無機陽イオンとの塩の析出を抑制できるが、地熱水には、無機陽イオンが大量に含まれているので、地熱水中の無機陽イオンの全てを除去しようとすると、処理コストがかさみ、地熱発電所の経済的な運用が困難であった。 On the other hand, as described in Patent Document 2, a salt of silica and an inorganic cation is obtained by injecting a scale-preventing agent into a production well and removing inorganic ions contained in geothermal water. However, geothermal water contains a large amount of inorganic cations, so if you try to remove all inorganic cations in the geothermal water, the treatment costs will increase and the economics of the geothermal power plant will increase. Operation was difficult.

　よって、本発明の目的は、カルシウムなどの無機陽イオンを含むスケールの抑制方法及び、これらのスケールの析出を抑制しつつ、経済的な運用が可能な地熱発電装置を提供することにある。 Therefore, an object of the present invention is to provide a method for suppressing a scale containing an inorganic cation such as calcium, and a geothermal power generation apparatus that can be economically operated while suppressing the precipitation of these scales.

　上記目的を達成するため、本発明のスケール抑制方法は、
　生産井から採取した地熱水の流量と、２価以上の無機陽イオン濃度を計測する流入水計測工程と、
　前記地熱水の熱を除去する熱除去工程と、
　前記熱除去工程後の地熱水の温度及びｐＨを計測する流出水計測工程と、
　前記熱除去工程後の地熱水の温度及びｐＨに基づいて、前記熱除去工程後の地熱水の無機陽イオンの飽和濃度を求め、前記流入水計測工程で測定した前記地熱水の無機陽イオン濃度から前記熱除去工程後の地熱水の無機陽イオンの飽和濃度を引いた値と、前記地熱水の流量とから、前記無機陽イオンを含む塩の析出を抑制するために必要なスケール抑制剤の添加量を演算するスケール抑制剤添加量演算工程と、
　前記スケール抑制剤添加量演算工程で演算されたスケール抑制剤の添加量に基づいて、前記生産井から採取した地熱水にスケール抑制剤を添加するスケール抑制剤添加工程とを含むことを特徴とする。 In order to achieve the above object, the scale suppression method of the present invention comprises:
An influent measurement process for measuring the flow rate of geothermal water collected from the production well and the concentration of inorganic cations of 2 or more,
A heat removal step of removing heat of the geothermal water;
An effluent measurement step for measuring the temperature and pH of the geothermal water after the heat removal step;
Based on the temperature and pH of the geothermal water after the heat removal step, the inorganic cation saturation concentration of the geothermal water after the heat removal step is obtained, and the inorganic of the geothermal water measured in the influent measurement step Necessary for suppressing precipitation of salt containing inorganic cation from the value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the heat removal step from the cation concentration and the flow rate of the geothermal water. A scale inhibitor addition amount calculating step for calculating the amount of the scale inhibitor added,
A scale inhibitor addition step of adding a scale inhibitor to geothermal water collected from the production well based on the addition amount of the scale inhibitor calculated in the scale inhibitor addition amount calculation step. To do.

　本発明のスケール抑制方法によれば、まず、生産井から採取した地熱水の流量と、２価以上の無機陽イオン濃度とを計測し、熱除去工程後の地熱水の温度及びｐＨを計測する。そして、熱除去工程後の地熱水の温度及びｐＨに基づいて、熱除去工程後の地熱水の無機陽イオンの飽和濃度を求め、流入水計測工程で測定した前熱水の無機陽イオン濃度から熱除去工程後の地熱水の無機陽イオンの飽和濃度を引いた値と、地熱水の流量とから、無機陽イオンを含む塩の析出を抑制するスケール抑制剤の添加量を演算する。こうして演算されたスケール抑制剤の添加量に基づいて、生産井から採取した地熱水にスケール抑制剤を添加する。これによって、熱除去工程後の地熱水において、飽和濃度以上となって析出する無機陽イオンの量に応じたスケール抑制剤を添加でき、スケールの析出を抑制できると共に、スケール抑制剤の添加量を必要最小限に抑えることができる。 According to the scale control method of the present invention, first, the flow rate of geothermal water collected from a production well and the concentration of divalent or higher inorganic cations are measured, and the temperature and pH of the geothermal water after the heat removal step are measured. measure. Then, based on the temperature and pH of the geothermal water after the heat removal step, the saturation concentration of the inorganic cation of the geothermal water after the heat removal step is obtained, and the inorganic cation of the preheated water measured in the influent measurement step Calculate the amount of scale inhibitor added to suppress the precipitation of salts containing inorganic cations from the concentration minus the saturation concentration of the inorganic cation after the heat removal step and the flow rate of the geothermal water. To do. Based on the calculated amount of the scale inhibitor added, the scale inhibitor is added to the geothermal water collected from the production well. As a result, in the geothermal water after the heat removal step, it is possible to add a scale inhibitor according to the amount of the inorganic cation that is deposited at a saturation concentration or higher, and it is possible to suppress the precipitation of scale, and the amount of the scale inhibitor added Can be minimized.

　本発明のスケール抑制方法は、前記生産井から採取した地熱水と同様なシリカ濃度及びｐＨで、前記無機陽イオン濃度を少しずつ増加させた試料水をそれぞれ作成し、前記各試料水を前記熱除去工程後の温度に所定時間保持した後、各処理水中の前記無機陽イオン濃度を測定し、前記試料水の無機陽イオン濃度よりも前記処理水の無機陽イオン濃度が最初に低くなるときの試料水の濃度を前記飽和濃度とすることが好ましい。 In the scale suppression method of the present invention, each of the sample waters is prepared by increasing the inorganic cation concentration little by little at the same silica concentration and pH as the geothermal water collected from the production well. After holding the temperature after the heat removal step for a predetermined time, when measuring the inorganic cation concentration in each treated water, when the inorganic cation concentration of the treated water first becomes lower than the inorganic cation concentration of the sample water It is preferable that the concentration of the sample water is the saturation concentration.

　この態様によれば、試料水の無機陽イオン濃度よりも前記処理水の無機陽イオン濃度が最初に低くなるときの試料水の無機陽イオン濃度を求めることにより、無機陽イオンを含む塩の析出が始まる飽和濃度を求めることができる。なお、シリカ濃度、ｐＨ、熱処理除去後の温度が変動する場合には、シリカ濃度、ｐＨ、熱除去工程後の温度を変えた様々な条件の下で上記飽和濃度を予め求めておくことにより、熱除去工程後の地熱水の温度及びｐＨに基づいて、熱除去工程後の地熱水の無機陽イオンの飽和濃度を求めることができる。 According to this aspect, by obtaining the inorganic cation concentration of the sample water when the inorganic cation concentration of the treated water first becomes lower than the inorganic cation concentration of the sample water, precipitation of the salt containing the inorganic cation is obtained. The saturation concentration at which can begin can be determined. In addition, when the silica concentration, pH, temperature after heat treatment removal varies, by obtaining the saturation concentration in advance under various conditions in which the silica concentration, pH, temperature after the heat removal step is changed, Based on the temperature and pH of the geothermal water after the heat removal step, the saturation concentration of the inorganic cation of the geothermal water after the heat removal step can be determined.

　本発明のスケール抑制方法は、前記無機陽イオンが、マグネシウムイオン、カルシウムイオン、２価の鉄イオン、３価の鉄イオン及びアルミニウムイオンから選ばれる一種以上であることが好ましい。上記無機陽イオンは、いずれもアルカリ条件下でシリカと反応して溶解しにくい塩を形成し、析出しやすいので、本発明の方法を適用する必要性が高いものである。 In the scale suppression method of the present invention, the inorganic cation is preferably at least one selected from magnesium ion, calcium ion, divalent iron ion, trivalent iron ion and aluminum ion. Any of the above inorganic cations reacts with silica under alkaline conditions to form a salt that is difficult to dissolve and is likely to precipitate, so that it is highly necessary to apply the method of the present invention.

　本発明のスケール抑制方法は、前記地熱水のｐＨを９以上に調整することが好ましい。地熱水のｐＨを９以上にすることによって、シリカの溶解度を高めてスケールの発生を抑制することができる。 In the scale suppression method of the present invention, it is preferable to adjust the pH of the geothermal water to 9 or more. By setting the pH of the geothermal water to 9 or more, it is possible to increase the solubility of silica and suppress the generation of scale.

　本発明のスケール抑制方法は、前記地熱水に、前記スケール抑制剤の添加と同時又は前記スケール抑制剤の添加後に、アルカリ剤を添加してｐＨを９以上に調整することが好ましい。地熱水に、スケール抑制剤の添加と同時又はスケール抑制剤の添加後に、アルカリ剤を添加してｐＨを９以上に調整することにより、アルカリ剤の添加における無機陽イオンによる塩の析出を防止することができる。 In the scale suppression method of the present invention, it is preferable to adjust the pH to 9 or more by adding an alkaline agent to the geothermal water simultaneously with the addition of the scale inhibitor or after the addition of the scale inhibitor. Simultaneously with the addition of the scale inhibitor to the geothermal water, or after the addition of the scale inhibitor, the alkaline agent is added to adjust the pH to 9 or more, thereby preventing salt precipitation due to inorganic cations in the addition of the alkaline agent. can do.

　本発明のスケール抑制方法の前記熱除去工程は、前記地熱水を減圧し、水蒸気を取出すフラッシュ工程及び／又は前記地熱水から熱を回収して発電媒体を蒸発させる工程を含むことが好ましい。この態様によれば、地熱水の熱を利用して発電を行うことができる。 The heat removal step of the scale suppression method of the present invention preferably includes a step of reducing the pressure of the geothermal water and taking out water vapor and / or a step of recovering heat from the geothermal water and evaporating the power generation medium. . According to this aspect, power generation can be performed using the heat of geothermal water.

　本発明のスケール抑制方法は、前記生産井から採取した地熱水を気液分離し、気液分離後の蒸気を発電設備に供給し、気液分離後の地熱水を前記熱除去工程に送ることが好ましい。この態様によれば、蒸気を分離した後の地熱水から更に熱を回収して、発電を行うことができる。 The scale suppression method of the present invention gas-liquid separates geothermal water collected from the production well, supplies steam after gas-liquid separation to a power generation facility, and uses the geothermal water after gas-liquid separation in the heat removal step. It is preferable to send. According to this aspect, heat can be further recovered from the geothermal water after separating the steam to generate power.

　また、本発明の地熱発電装置は、
　生産井から採取される地熱水中の２価以上の無機陽イオン濃度を測定する無機陽イオン濃度測定装置と、
　前記生産井から採取される地熱水の流量を測定する流量計と、
　前記地熱水の温度を低下させる熱除去部と、
　前記熱除去後の地熱水の温度を測定する温度計と、
　前記熱除去後の地熱水のｐＨを計測するｐＨ測定装置と、
　前記熱除去部で温度を低下させた後の地熱水の温度及びｐＨに基づいて、前記熱除去部で温度を低下させた後の地熱水の無機陽イオンの飽和濃度を求め、前記無機陽イオン濃度測定装置で測定した前記地熱水の無機陽イオン濃度から前記熱除去部で温度を低下させた後の地熱水の無機陽イオンの飽和濃度を引いた値と、前記地熱水の流量とから、前記無機陽イオンを含む塩の析出を抑制するために必要なスケール抑制剤の添加量を算出する演算処理部と、
　前記地熱水に、前記演算処理部で算出された量のスケール抑制剤を添加する制御部とを備えていることを特徴とする。 Moreover, the geothermal power generator of the present invention is
An inorganic cation concentration measuring device that measures the concentration of divalent or higher inorganic cations in geothermal water collected from production wells;
A flow meter for measuring the flow rate of geothermal water collected from the production well;
A heat removal section for lowering the temperature of the geothermal water;
A thermometer for measuring the temperature of the geothermal water after the heat removal;
A pH measuring device for measuring the pH of the geothermal water after the heat removal;
Based on the temperature and pH of the geothermal water after the temperature is lowered at the heat removal unit, the saturation concentration of the inorganic cation of the geothermal water after the temperature is lowered at the heat removal unit is determined, and the inorganic A value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the temperature has been lowered by the heat removal unit from the inorganic cation concentration of the geothermal water measured by a cation concentration measuring device, and the geothermal water From the flow rate of, the arithmetic processing unit that calculates the amount of scale inhibitor added to suppress precipitation of the salt containing the inorganic cation,
And a control unit that adds the amount of the scale inhibitor calculated by the arithmetic processing unit to the geothermal water.

　本発明の地熱発電装置によれば、演算処理部において、前記温度計によって測定した温度と、前記ｐＨ測定装置によって測定したｐＨに基づいて、前記熱除去部で温度を低下させた後の地熱水の無機陽イオンの飽和濃度を求める。次いで、前記無機陽イオン濃度測定装置によって測定した無機陽イオン濃度から上記飽和濃度を差し引いた値と、前記流量計によって測定した流量とから、そのままでは析出すると予測される無機陽イオン量を算出し、その量の無機陽イオンの析出を抑制するに必要なスケール抑制剤の添加量を算出する。そして、制御部において、上記演算処理部で算出された量のスケール抑制剤を添加することにより、スケールの析出を抑制しつつ、スケール抑制剤の添加量を必要最小限に抑えることができる。 According to the geothermal power generation device of the present invention, in the arithmetic processing unit, the geothermal heat after the temperature is reduced by the heat removal unit based on the temperature measured by the thermometer and the pH measured by the pH measurement device. Obtain the saturated concentration of inorganic cations in water. Next, from the value obtained by subtracting the saturation concentration from the inorganic cation concentration measured by the inorganic cation concentration measuring device and the flow rate measured by the flow meter, the amount of inorganic cation that is expected to precipitate as it is is calculated. The amount of the scale inhibitor added to suppress the precipitation of that amount of inorganic cation is calculated. In the control unit, by adding the amount of the scale inhibitor calculated by the arithmetic processing unit, the amount of the scale inhibitor added can be minimized while suppressing the precipitation of scale.

　本発明の地熱発電装置は、前記熱除去部の前段に、気液分離器が配置され、気液分離後の地熱水を前記熱除去部に導入するように構成されていることが好ましい。この態様によれば、地熱水から発電用の蒸気を採取した後の地熱水を利用して、更に熱回収を行うことができる。 The geothermal power generation apparatus of the present invention is preferably configured so that a gas-liquid separator is disposed in front of the heat removal unit, and geothermal water after gas-liquid separation is introduced into the heat removal unit. According to this aspect, heat recovery can be further performed using the geothermal water after collecting steam for power generation from the geothermal water.

　本発明の地熱発電装置の前記熱除去部は、放熱する配管、減圧により地熱水から蒸気を取出すフラッシャー及び発電媒体に熱を与えて発電媒体を蒸発させる熱交換器から選ばれる１種以上であることが好ましい。この態様によれば、地熱水から蒸気を分離して蒸気タービンにより発電を行ったり、地熱水の熱により発電媒体を蒸発させて、発電を行うことができる。 The heat removal unit of the geothermal power generation apparatus of the present invention is one or more types selected from a heat radiating pipe, a flasher that extracts steam from geothermal water by decompression, and a heat exchanger that heats the power generation medium to evaporate the power generation medium. Preferably there is. According to this aspect, it is possible to generate power by separating steam from geothermal water and generating power by a steam turbine, or by evaporating a power generation medium by the heat of geothermal water.

　本発明の地熱発電装置は、試料水を貯留する溶液貯留部と、この溶液貯留部に貯留された試料水の温度を調整する温度制御部と、前記溶液貯留部に貯留された試料水に酸又はアルカリを添加して、ｐＨを調整するｐＨ調整部と、所定時間経過後に試料水中の２価以上の無機陽イオン濃度を測定する濃度計測部と、試料水として前記無機陽イオン濃度を徐々に高めたものを作成して順次、前記溶液貯留部に流入させる溶液供給部とを有する無機陽イオンの飽和濃度測定装置を備えていることが好ましい。この態様によれば、試料水のｐＨ、温度を変えて、様々なｐＨ及び温度条件下における無機陽イオンの飽和濃度を予め測定することができるので、地熱水の温度やｐＨを測定することにより、その地熱水における無機陽イオンの飽和濃度を求めることができる。 The geothermal power generation apparatus of the present invention includes a solution storage unit that stores sample water, a temperature control unit that adjusts the temperature of the sample water stored in the solution storage unit, and an acid in the sample water stored in the solution storage unit. Alternatively, a pH adjusting unit for adjusting pH by adding alkali, a concentration measuring unit for measuring a divalent or higher valent inorganic cation concentration in a sample water after a predetermined time, and gradually adjusting the inorganic cation concentration as sample water It is preferable to provide a saturation concentration measuring device for an inorganic cation having a solution supply unit that creates an enhanced one and sequentially flows into the solution storage unit. According to this aspect, since the saturation concentration of inorganic cations under various pH and temperature conditions can be measured in advance by changing the pH and temperature of the sample water, the temperature and pH of the geothermal water can be measured. Thus, the saturation concentration of the inorganic cation in the geothermal water can be obtained.

　本発明のスケール抑制方法によれば、前述したように、スケール抑制剤添加量演算工程で演算されたスケール抑制剤の添加量に基づいて、生産井から採取した地熱水にスケール抑制剤を添加するので、熱除去工程後の地熱水において、飽和濃度以上となって析出する無機陽イオンの量に応じたスケール抑制剤を添加でき、スケールの析出を抑制できると共に、スケール抑制剤の添加量を必要最小限に抑えることができる。 According to the scale suppression method of the present invention, as described above, based on the scale inhibitor addition amount calculated in the scale inhibitor addition amount calculation step, the scale inhibitor is added to the geothermal water collected from the production well. Therefore, in the geothermal water after the heat removal step, it is possible to add a scale inhibitor according to the amount of the inorganic cation deposited at a saturation concentration or more, and suppress the precipitation of the scale, and the addition amount of the scale inhibitor Can be minimized.

　また、本発明の地熱発電装置によれば、演算処理部において、そのままでは析出すると予測される無機陽イオン量を算出し、その量の無機陽イオンの析出を抑制するに必要なスケール抑制剤の添加量を算出して、制御部において、上記演算処理部で算出された量のスケール抑制剤を添加することにより、スケールの析出を抑制しつつ、スケール抑制剤の添加量を必要最小限に抑えることができ、発電装置の経済的な運用ができる。 Further, according to the geothermal power generation apparatus of the present invention, the arithmetic processing unit calculates the amount of inorganic cations that are predicted to precipitate as they are, and the scale inhibitor necessary for suppressing the precipitation of the inorganic cations of that amount. By calculating the addition amount and adding the amount of the scale inhibitor calculated by the arithmetic processing unit in the control unit, the amount of the scale inhibitor added is minimized while suppressing the precipitation of scale. The power generator can be operated economically.

本発明による地熱発電装置の一実施形態を示す概略構成図である。It is a schematic block diagram which shows one Embodiment of the geothermal power generator by this invention. 本発明で用いる無機陽イオンの飽和濃度測定装置の一例を示す概略構成図である。It is a schematic block diagram which shows an example of the saturated concentration measuring apparatus of the inorganic cation used by this invention. 本発明において無機陽イオンの飽和濃度を測定する方法の一例を示す工程図である。It is process drawing which shows an example of the method of measuring the saturated concentration of an inorganic cation in this invention. 本発明の方法により特定条件におけるカルシウムイオンの飽和濃度を測定した結果を示す図表である。It is a graph which shows the result of having measured the saturation density | concentration of the calcium ion in specific conditions by the method of this invention. 溶液のｐＨとカルシウムシリケートの飽和濃度との関係を示す図表である。It is a graph which shows the relationship between pH of a solution, and the saturation density | concentration of a calcium silicate. 本発明の一実施形態によりスケール抑制剤を添加する工程を示す図表である。It is a graph which shows the process of adding a scale inhibitor by one Embodiment of this invention.

　本発明の地熱発電装置の一実施形態について、図１を参照して説明する。 An embodiment of the geothermal power generation apparatus of the present invention will be described with reference to FIG.

　図１において、生産井１０から採取された地熱水は、配管Ｌ１を通してセパレータ１１に送られる。セパレータ１１では、熱水と蒸気とが分離されて、蒸気は、配管Ｌ３を経て第１タービン１２に送られ、第１発電機１３による発電がなされる。セパレータ１１は熱水を減圧して蒸気を取出すフラッシャーの機能を有する。なお、第１タービン１２を通過した蒸気は、配管Ｌ４を経て復水器１４に送られて凝縮水となり、更に配管Ｌ５を経て冷却塔１５に送られて冷却され、図示しない経路を通って還元井１６に戻される。なお、冷却塔１５で冷却された水の一部は、配管Ｌ６を介して復水器１４に戻され、第１タービン１２から送られてくる蒸気の冷却水として使用される。 1, geothermal water collected from the production well 10 is sent to the separator 11 through the pipe L1. In the separator 11, hot water and steam are separated, and the steam is sent to the first turbine 12 via the pipe L <b> 3, and power is generated by the first generator 13. The separator 11 has a function of a flasher for extracting steam by depressurizing hot water. The steam that has passed through the first turbine 12 is sent to the condenser 14 via the pipe L4 to become condensed water, further sent to the cooling tower 15 via the pipe L5, cooled, and reduced through a path (not shown). Returned to the well 16. A part of the water cooled by the cooling tower 15 is returned to the condenser 14 via the pipe L6 and used as cooling water for the steam sent from the first turbine 12.

　この実施形態では、セパレータ１１で蒸気と分離された地熱水から更に熱回収すると共に、熱回収した地熱水を還元井１６に戻す間に無機陽イオンとシリカとが反応してスケールとして析出するのを防止するようにしている。すなわち、この実施形態では、セパレータ１１で蒸気と分離された地熱水が、本発明における生産井から採取した地熱水に相当する。ただし、本発明では、生産井１０から採取した地熱水をそのまま、以下に述べる媒体蒸発器１７に供するようにしてもよい。 In this embodiment, the heat is further recovered from the geothermal water separated from the steam by the separator 11, and the inorganic cation reacts with the silica and precipitates as a scale while the recovered geothermal water is returned to the reduction well 16. I try to prevent it. That is, in this embodiment, the geothermal water separated from the steam by the separator 11 corresponds to the geothermal water collected from the production well in the present invention. However, in the present invention, the geothermal water collected from the production well 10 may be used as it is for the medium evaporator 17 described below.

　この媒体蒸発器を備えた地熱発電装置は、セパレータ１１で分離された地熱水の熱を利用して、バイナリー発電を行うものである。すなわち、セパレータ１１で分離された地熱水は、配管Ｌ７を介して媒体蒸発器１７に送られ、ここで熱交換して低沸点の熱媒体を蒸発させた後、配管Ｌ８を介して還元井１６に戻されるようになっている。この実施形態では、媒体蒸発器１７が、本発明における熱除去部に相当する。 The geothermal power generation apparatus equipped with this medium evaporator performs binary power generation using the heat of the geothermal water separated by the separator 11. That is, the geothermal water separated by the separator 11 is sent to the medium evaporator 17 via the pipe L7, where heat exchange is performed to evaporate the low boiling point heat medium, and then the reduction well is connected via the pipe L8. 16 is returned. In this embodiment, the medium evaporator 17 corresponds to the heat removal unit in the present invention.

　媒体蒸発器１７で気化された熱媒体は、配管Ｌ９を介して第２タービン１８に送られ、第２発電機１９による発電がなされる。更に、第２タービン１８を通過した熱媒体は、配管Ｌ１０を介して媒体凝縮器２０に送られ、ここで凝縮液となって、更に途中にポンプ２１を有する配管Ｌ１１を介して、媒体蒸発器１７に戻されるようになっている。 The heat medium vaporized by the medium evaporator 17 is sent to the second turbine 18 through the pipe L9, and the second generator 19 generates power. Furthermore, the heat medium that has passed through the second turbine 18 is sent to the medium condenser 20 via the pipe L10, where it becomes a condensate, and further passes through the pipe L11 having the pump 21 in the middle, to the medium evaporator. 17 is returned.

　このバイナリー発電における熱媒体としては、セパレータ１１で分離された地熱水の熱を利用して気化することが可能な低沸点の熱媒体が用いられ、特に限定されないが、例えば、ノルマルヘプタン、イソヘプタン、ノルマルペンタン、イソペンタン、ノルマルブタン、イソブタン、ハイドロフルオロエーテル、Ｒ２４５ｆａ、Ｒ１３４ａ、Ｒ２２、Ｒ４０７ｃなどが好適に用いられる。 As the heat medium in this binary power generation, a low-boiling-point heat medium that can be vaporized using the heat of the geothermal water separated by the separator 11 is used, and is not particularly limited. For example, normal heptane, isoheptane , Normal pentane, isopentane, normal butane, isobutane, hydrofluoroether, R245fa, R134a, R22, R407c, and the like are preferably used.

　上記のように、セパレータ１１で分離された地熱水は、媒体蒸発器１７を通って熱回収された後、還元井１６に戻されるのであるが、その間に温度低下して、シリカを主成分とするスケールが発生し、配管を閉塞させるという問題があった。これに対して、前述したように、アルカリ剤を添加してアルカリ性にすることにより、非晶質シリカの溶解度を高めることが考えられるが、アルカリ性にすると、２価以上の無機陽イオンとシリカとが塩を形成して析出しやすくなるという別の問題が発生する。 As described above, the geothermal water separated by the separator 11 is recovered by heat through the medium evaporator 17 and then returned to the reduction well 16. There was a problem that the scale was generated and the piping was blocked. On the other hand, as described above, it is conceivable to increase the solubility of amorphous silica by adding an alkali agent to make it alkaline, but if it is made alkaline, divalent or higher inorganic cations and silica Another problem arises in that it forms a salt and tends to precipitate.

　そこで、本発明では、地熱水中に含まれる２価以上の無機陽イオンの濃度に応じて、スケール抑制剤を添加して、無機陽イオンとシリカとの塩によるスケールの発生を抑制するようにする。 Therefore, in the present invention, a scale inhibitor is added in accordance with the concentration of the divalent or higher valent inorganic cation contained in the geothermal water to suppress the generation of scale due to the salt of the inorganic cation and silica. .

　なお、本発明において、２価以上の無機陽イオンとしては、特に限定されるものではないが、例えばマグネシウムイオン、カルシウムイオン、２価の鉄イオン、３価の鉄イオン及びアルミニウムイオンから選ばれる一種以上が挙げられる。また、スケール抑制剤としては、例えば、ＥＤＴＡ、ＮＴＡ（ニトリロ三酢酸）、ＨＩＤＳ（３－ヒドロキシ－２－２’－イミノジコハク酸)、カルボキシメチルエチレンイミン、クエン酸、酒石酸及びそれらの各種ナトリウム塩、カリウム塩、アンモニウム塩、水和物などのキレート剤、ＰＡＳ（ポリアクリル酸Ｎａ）などが挙げられる。 In the present invention, the divalent or higher valent inorganic cation is not particularly limited. For example, it is a kind selected from magnesium ion, calcium ion, divalent iron ion, trivalent iron ion and aluminum ion. The above is mentioned. Examples of the scale inhibitor include EDTA, NTA (nitrilotriacetic acid), HIDS (3-hydroxy-2-2′-iminodisuccinic acid), carboxymethylethyleneimine, citric acid, tartaric acid, and various sodium salts thereof. Chelating agents such as potassium salts, ammonium salts and hydrates, PAS (polyacrylic acid Na) and the like.

　図１に基づいて、上記のようなスケール抑制方法を実施するための装置構成について説明すると、セパレータ１１から媒体蒸発器１７に至る配管Ｌ７には、無機陽イオン濃度計２２及びシリカ濃度計２３が接続されている。また、シリカ濃度計の下流には、アルカリ剤タンク２４内のアルカリ剤がポンプ２５を介して流入するようになっており、それとほぼ同じ箇所に、キレート剤タンク２６内のキレート剤がポンプ２７を介して流入するようになっている。アルカリ剤の流入箇所は、キレート剤の流入箇所と同じか、あるいはキレート剤の流入箇所よりも下流側であることが好ましい。 An apparatus configuration for carrying out the above-described scale suppression method will be described with reference to FIG. 1. An inorganic cation concentration meter 22 and a silica concentration meter 23 are provided in a pipe L 7 extending from the separator 11 to the medium evaporator 17. It is connected. Further, the alkaline agent in the alkaline agent tank 24 flows into the downstream of the silica concentration meter via the pump 25, and the chelating agent in the chelating agent tank 26 is connected to the pump 27 at almost the same location. It comes to flow in through. The inflow site of the alkaline agent is preferably the same as the inflow site of the chelating agent or downstream of the inflow site of the chelating agent.

　アルカリ剤タンク２４から供給されるアルカリ剤の添加量は、地熱水のｐＨを好ましくは９以上、より好ましくは９．５～１０．０になるように調整される。 The addition amount of the alkaline agent supplied from the alkaline agent tank 24 is adjusted so that the pH of the geothermal water is preferably 9 or more, more preferably 9.5 to 10.0.

　また、キレート剤の添加量は、演算処理部２８からの信号を受けて、キレート剤添加量制御部２９によって、ポンプ２７を制御することによって調整されるようになっている。 Further, the addition amount of the chelating agent is adjusted by receiving the signal from the arithmetic processing unit 28 and controlling the pump 27 by the chelating agent addition amount control unit 29.

　配管Ｌ７のアルカリ剤の流入箇所よりも更に下流側には、流量計３０が接続されており、媒体蒸発器１７に流入する地熱水の流量を測定できるようなっている。なお、流量計３０の設置箇所は、上記箇所に限られず、アルカリ剤やキレート剤の添加箇所よりも上流側であってもよい。 A flow meter 30 is connected further downstream of the inflow point of the alkaline agent in the pipe L7 so that the flow rate of the geothermal water flowing into the medium evaporator 17 can be measured. In addition, the installation location of the flow meter 30 is not limited to the above location, and may be upstream of the location where the alkali agent or chelating agent is added.

　媒体蒸発器１７と還元井１６を連結する配管Ｌ８には、温度計３１とｐＨ計３２とが接続されており、媒体蒸発器１７を経て還元井に戻される地熱水の温度やｐＨを測定するようになっている。なお、無機陽イオン濃度計２２、シリカ濃度計２３、流量計３０、温度計３１及びｐＨ計３２は、それぞれ演算処理部２８に接続されている。また、演算処理部２８には、記憶装置３３が接続され、記憶装置３３には入力装置３４が接続されている。 A thermometer 31 and a pH meter 32 are connected to the pipe L8 connecting the medium evaporator 17 and the reduction well 16, and the temperature and pH of the geothermal water returned to the reduction well through the medium evaporator 17 are measured. It is supposed to be. The inorganic cation concentration meter 22, the silica concentration meter 23, the flow meter 30, the thermometer 31, and the pH meter 32 are each connected to the arithmetic processing unit 28. Further, a storage device 33 is connected to the arithmetic processing unit 28, and an input device 34 is connected to the storage device 33.

　図２には、本発明で好適に用いられる無機陽イオンの飽和濃度測定装置の一例が示されている。この無機陽イオンの飽和濃度測定装置４０は、溶液貯留部４１を有し、この溶液貯留部４１に、温度制御部４２と、溶液採取部４３と、ｐＨ調整部４４と、陽イオン濃度計測部４５とが接続されている。ｐＨ調整部４４には、ｐＨ測定部４４ａ及び酸アルカリ添加部４４ｂが設けられている。陽イオン濃度計測部４５には、タイマ４５ａが取付けられている。 FIG. 2 shows an example of an inorganic cation saturation concentration measuring apparatus suitably used in the present invention. The inorganic cation saturation concentration measuring device 40 includes a solution storage unit 41. The solution storage unit 41 includes a temperature control unit 42, a solution collection unit 43, a pH adjustment unit 44, and a cation concentration measurement unit. 45 is connected. The pH adjusting unit 44 is provided with a pH measuring unit 44a and an acid / alkali adding unit 44b. A timer 45 a is attached to the cation concentration measuring unit 45.

　図３には、上記飽和濃度測定装置４０を用いて、無機陽イオンの飽和濃度を測定するフローチャートが示されている。この実施形態では、無機陽イオンとしてカルシウムイオンを選択し、カルシウムシリケートの析出開始点（飽和濃度）を求めている。 FIG. 3 shows a flowchart for measuring the saturation concentration of the inorganic cation using the saturation concentration measuring device 40. In this embodiment, calcium ion is selected as the inorganic cation, and the precipitation start point (saturation concentration) of calcium silicate is obtained.

　すなわち、まず、シリカ濃度を６００ｍｇ／Ｌとし、カルシウム濃度を０～５０ｍｇ／Ｌの範囲で徐々所に高めた反応液を調整し、溶液採取部４３を通して、溶液貯留部４１に充填する（ステップＳ１）。 That is, first, a reaction solution in which the silica concentration is 600 mg / L and the calcium concentration is gradually increased in the range of 0 to 50 mg / L is prepared, and the solution storage unit 41 is filled through the solution collecting unit 43 (step S1). ).

　次いで、ｐＨ調整部４４のｐＨ測定部４４ａにてｐＨを測定しながら、酸アルカリ添加部４４ｂから、例えば、塩酸又は水酸化ナトリウム水溶液を添加して、所定のｐＨ、例えばｐＨ９，１０，１１となるように調整する（ステップＳ２）。 Next, while measuring the pH by the pH measuring unit 44a of the pH adjusting unit 44, for example, hydrochloric acid or a sodium hydroxide aqueous solution is added from the acid-alkali adding unit 44b, and a predetermined pH, for example, pH 9, 10, 11 It adjusts so that it may become (step S2).

　こうして所定のカルシウム濃度及びｐＨに調整された反応液を、所定の条件、この実施形態では１００℃、３時間という条件で恒温保持する（ステップＳ３）。この条件は、媒体蒸発器１７を通って還元井１６に戻されるときの温度や時間と同様になるように設定することが好ましい。 Thus, the reaction liquid adjusted to a predetermined calcium concentration and pH is kept at a constant temperature under predetermined conditions, in this embodiment, 100 ° C. for 3 hours (step S3). This condition is preferably set to be the same as the temperature and time when returning to the reduction well 16 through the medium evaporator 17.

　次いで、タイマ４５ａにて所定時間（この実施形態では３時間）経過したら、陽イオン濃度計測部４５により陽イオン濃度（この実施形態ではカルシウム濃度）を測定する（ステップＳ４）。カルシウム濃度は、例えば、ＥＤＴＡ滴定やカルシウムイオン計で測定することができる。 Next, when a predetermined time (3 hours in this embodiment) has elapsed in the timer 45a, the cation concentration measurement unit 45 measures the cation concentration (calcium concentration in this embodiment) (step S4). The calcium concentration can be measured by, for example, EDTA titration or a calcium ion meter.

　そして、最初に添加したカルシウムイオン濃度が、反応後のカルシウムイオン濃度よりも高いかどうかを判断し（ステップＳ５）、ＮＯの場合は、ステップＳ１に戻る。また、ＹＥＳの場合は、そのときの試料水のカルシウムイオン濃度（ステップＳ１での濃度）を析出開始点（本発明における飽和濃度）と判定し（ステップＳ６）、終了する。 Then, it is determined whether or not the initially added calcium ion concentration is higher than the calcium ion concentration after the reaction (step S5). If NO, the process returns to step S1. In the case of YES, the calcium ion concentration of the sample water at that time (concentration in step S1) is determined as the deposition start point (saturated concentration in the present invention) (step S6), and the process is terminated.

　なお、カルシウムに限らず、例えばマグネシウムの場合には、ステップＳ１でマグネシウムの濃度を徐々に増加させた反応液を調整して、同様な測定を行えばよい。 It should be noted that, in addition to calcium, for example, in the case of magnesium, a similar measurement may be performed by adjusting a reaction solution in which the concentration of magnesium is gradually increased in step S1.

　図４には、上記方法でｐＨ９でカルシウムの飽和濃度を測定した結果が示されており、同図の横軸は、反応液調整時のカルシウム添加量（ｍｇ／Ｌ）を示し、縦軸は、反応後のカルシウムイオン濃度（ｍｇ／Ｌ、黒四角のグラフ）、及び同カルシウム添加量から反応後のカルシウムイオン濃度を引いた値（ｍｇ／Ｌ、黒三角のグラフ）を示している。したがって、シリカ濃度を６００ｍｇ／Ｌとし、ｐＨ９で、１００℃、３時間の処理を行った場合のカルシウムイオンの飽和濃度は、カルシウム添加量から反応後のカルシウムイオン濃度を引いた値が正の値に転じるカルシウム添加量である５ｍｇ／Ｌとなる。 FIG. 4 shows the result of measuring the saturation concentration of calcium at pH 9 by the above method, where the horizontal axis indicates the amount of calcium added (mg / L) during reaction liquid adjustment, and the vertical axis indicates , The calcium ion concentration after reaction (mg / L, black square graph), and the value obtained by subtracting the calcium ion concentration after reaction from the same calcium addition amount (mg / L, black triangle graph) are shown. Therefore, when the silica concentration is 600 mg / L, and the treatment is performed at 100 ° C. for 3 hours at pH 9, the value obtained by subtracting the calcium ion concentration after reaction from the calcium addition amount is a positive value. 5 mg / L, which is the amount of calcium added to turn to 1.

　図５には、各種ｐＨ条件下で図３に示した測定を繰り返して、それぞれのｐＨにおけるカルシウムの飽和濃度を測定した結果が示されている。このようにｐＨが上昇するにつれて、カルシウムの飽和濃度が低下することがわかる。 FIG. 5 shows the results of measuring the saturation concentration of calcium at each pH by repeating the measurement shown in FIG. 3 under various pH conditions. Thus, it turns out that the saturation concentration of calcium falls as pH rises.

　こうして、媒体蒸発器１７を通って還元井１６に戻されるときの温度や時間と同様になるように設定された所定の条件で処理した場合の、各無機陽イオンの飽和濃度について、ｐＨを変えて測定したデータを予め求めておき、そのデータを図１の入力装置３４から記憶装置３３に入力して格納しておく。なお、上記温度や時間が変動する場合は、各種の条件で上記データを求めておく。 In this way, the pH is changed with respect to the saturation concentration of each inorganic cation when processing is performed under predetermined conditions set to be similar to the temperature and time when returning to the reduction well 16 through the medium evaporator 17. The data measured in advance is obtained in advance, and the data is input from the input device 34 of FIG. 1 to the storage device 33 and stored. When the temperature and time fluctuate, the data is obtained under various conditions.

　次に、図１の演算処理部２８で、スケール抑制剤であるキレート剤の添加量を求め、キレート剤添加量制御部２９によりポンプ２７を制御して、所定量のキレート剤を添加する手順について、図６を参照して説明する。 Next, the calculation processing unit 28 in FIG. 1 calculates the addition amount of the chelating agent that is a scale inhibitor, and controls the pump 27 by the chelating agent addition amount control unit 29 to add a predetermined amount of the chelating agent. This will be described with reference to FIG.

　まず、温度計３１で測定された温度と、ｐＨ計３２によって測定されたｐＨに基づいて、記憶装置３３に格納された、各種条件下での各無機陽イオンの飽和濃度のデータから、上記測定された条件下における、地熱水中の無機陽イオンの飽和濃度を決定する（ステップＳ１）。 First, based on the temperature measured by the thermometer 31 and the pH measured by the pH meter 32, the above measurement is performed from the data of the saturated concentration of each inorganic cation stored in the storage device 33 under various conditions. The saturation concentration of the inorganic cation in the geothermal water under the determined conditions is determined (step S1).

　次いで、無機陽イオン濃度計２２で測定された、地熱水の無機陽イオン濃度から、上記で決定された飽和濃度を引いた値を算出する（ステップＳ１２）。ここでセパレータ１１により地熱水を蒸発させて蒸気を得る場合には、地熱水中の無機陽イオン濃度が上昇するため、蒸発量から濃縮率を推定し地熱水の無機陽イオン濃度とする。 Next, a value obtained by subtracting the saturation concentration determined above from the inorganic cation concentration of the geothermal water measured by the inorganic cation concentration meter 22 is calculated (step S12). Here, when the vapor is obtained by evaporating the geothermal water by the separator 11, the concentration of the inorganic cation in the geothermal water increases, so the concentration rate is estimated from the amount of evaporation to obtain the inorganic cation concentration of the geothermal water.

　次いで、流量計３０で測定された地熱水の流量と、上記地熱水の無機陽イオン濃度から飽和濃度を引いた値とから、スケール抑制剤（キレート剤）を添加しなかった場合に予測される、スケールとして析出する無機陽イオンの量を算出する（ステップＳ１３）。 Next, prediction is made when a scale inhibitor (chelating agent) is not added from the flow rate of the geothermal water measured by the flow meter 30 and the value obtained by subtracting the saturation concentration from the inorganic cation concentration of the geothermal water. The amount of inorganic cations deposited as scale is calculated (step S13).

　次いで、上記予測される析出量の無機陽イオンの析出を抑制するために必要なスケール抑制剤（キレート剤）の添加量を算出する（ステップＳ１４）。 Next, the addition amount of a scale inhibitor (chelating agent) necessary for suppressing the precipitation of the inorganic cation having the predicted precipitation amount is calculated (step S14).

　最後に、キレート剤添加量制御部２９に信号を送り、上記で求められた添加量となるようにポンプ２７を作動させて、スケール抑制剤を添加し（ステップＳ１５）、ルーチンを終了する。 Finally, a signal is sent to the chelating agent addition amount control unit 29, the pump 27 is operated so as to obtain the addition amount obtained above, the scale inhibitor is added (step S15), and the routine is terminated.

　上記演算処理部２８による図６の操作は、例えば所定時間毎に行い、地熱水中に常に適切な量の析出抑制剤が添加されるようにする。 The operation of FIG. 6 by the arithmetic processing unit 28 is performed, for example, every predetermined time so that an appropriate amount of precipitation inhibitor is always added to the geothermal water.

　こうして、地熱水が配管中でスケールを析出するのを防止しつつ、第１タービン１２による第１発電機１３での発電と、第２タービン１８による第２発電機１９での発電とを行い、地熱水の熱エネルギーを有効利用して発電を行うことが可能となる。また、スケール析出抑制剤（キレート剤）の添加量を必要最小限に抑えることができるので、経済的な運転が可能となる。 In this way, while preventing the geothermal water from depositing scale in the pipe, the first turbine 12 generates power with the first generator 13 and the second turbine 18 generates power with the second generator 19. In addition, it is possible to generate electricity by effectively using the thermal energy of geothermal water. Moreover, since the addition amount of the scale precipitation inhibitor (chelating agent) can be suppressed to the minimum necessary, economical operation becomes possible.

１０　生産井
１１　セパレータ
１２　第１タービン
１３　第１発電機
１７　媒体蒸発器
１８　第２タービン
１９　第２発電機
２０　媒体凝縮器
２１　ポンプ
２２　無機陽イオン濃度計
２３　シリカ濃度計
２４　アルカリ剤タンク
２５　ポンプ
２６　キレート剤タンク
２７　ポンプ
２８　演算処理部
２９　キレート剤添加量制御部
３０　流量計
３１　温度計
３２　ｐＨ計
３３　記憶装置
３４　入力装置
４０　飽和濃度測定装置
４１　溶液貯留部
４２　温度制御部
４３　溶液採取部
４４　ｐＨ調整部
４４ａ　ｐＨ測定部
４４ｂ　酸アルカリ添加部
４５　陽イオン濃度計測部
４５ａ　タイマ DESCRIPTION OF SYMBOLS 10 Production well 11 Separator 12 1st turbine 13 1st generator 17 Medium evaporator 18 2nd turbine 19 2nd generator 20 Medium condenser 21 Pump 22 Inorganic cation concentration meter 23 Silica concentration meter 24 Alkali agent tank 25 Pump 26 Chelating agent tank 27 Pump 28 Arithmetic processing unit 29 Chelating agent addition amount control unit 30 Flow meter 31 Thermometer 32 pH meter 33 Storage device 34 Input device 40 Saturation concentration measuring device 41 Solution storage unit 42 Temperature control unit 43 Solution sampling unit 44 pH Adjustment unit 44a pH measurement unit 44b Acid / alkali addition unit 45 Cation concentration measurement unit 45a Timer

Claims (11)

　生産井から採取した地熱水の流量と、２価以上の無機陽イオン濃度を計測する流入水計測工程と、
　前記地熱水の熱を除去する熱除去工程と、
　前記熱除去工程後の地熱水の温度及びｐＨを計測する流出水計測工程と、
　前記熱除去工程後の地熱水の温度及びｐＨに基づいて、前記熱除去工程後の地熱水の無機陽イオンの飽和濃度を求め、前記流入水計測工程で測定した前記地熱水の無機陽イオン濃度から前記熱除去工程後の地熱水の無機陽イオンの飽和濃度を引いた値と、前記地熱水の流量とから、前記無機陽イオンを含む塩の析出を抑制するために必要なスケール抑制剤の添加量を演算するスケール抑制剤添加量演算工程と、
　前記スケール抑制剤添加量演算工程で演算されたスケール抑制剤の添加量に基づいて、前記生産井から採取した地熱水にスケール抑制剤を添加するスケール抑制剤添加工程とを含むことを特徴とするスケール抑制方法。 An influent measurement process for measuring the flow rate of geothermal water collected from the production well and the concentration of inorganic cations of 2 or more,
A heat removal step of removing heat of the geothermal water;
An effluent measurement step for measuring the temperature and pH of the geothermal water after the heat removal step;
Based on the temperature and pH of the geothermal water after the heat removal step, the inorganic cation saturation concentration of the geothermal water after the heat removal step is obtained, and the inorganic of the geothermal water measured in the influent measurement step Necessary for suppressing precipitation of salt containing inorganic cation from the value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the heat removal step from the cation concentration and the flow rate of the geothermal water. A scale inhibitor addition amount calculating step for calculating the amount of the scale inhibitor added,
A scale inhibitor addition step of adding a scale inhibitor to geothermal water collected from the production well based on the addition amount of the scale inhibitor calculated in the scale inhibitor addition amount calculation step. How to suppress scale. 　前記生産井から採取した地熱水と同様なシリカ濃度及びｐＨで、前記無機陽イオン濃度を少しずつ増加させた試料水をそれぞれ作成し、
　前記各試料水を前記熱除去工程後の温度に所定時間保持した後、各処理水中の前記無機陽イオン濃度を測定し、
　前記試料水の無機陽イオン濃度よりも前記処理水の無機陽イオン濃度が最初に低くなるときの試料水の濃度を前記飽和濃度とする請求項１に記載のスケール抑制方法。 Sample water in which the inorganic cation concentration is increased little by little at the same silica concentration and pH as the geothermal water collected from the production well,
After holding each sample water at the temperature after the heat removal step for a predetermined time, measure the inorganic cation concentration in each treated water,
The scale suppression method according to claim 1, wherein the concentration of the sample water when the inorganic cation concentration of the treated water is initially lower than the inorganic cation concentration of the sample water is the saturation concentration. 　前記無機陽イオンが、マグネシウムイオン、カルシウムイオン、２価の鉄イオン、３価の鉄イオン及びアルミニウムイオンから選ばれる一種以上である請求項１に記載のスケール抑制方法。 The scale suppression method according to claim 1, wherein the inorganic cation is one or more selected from magnesium ion, calcium ion, divalent iron ion, trivalent iron ion and aluminum ion. 　前記地熱水のｐＨを９以上に調整する請求項１～３のいずれか１つに記載のスケール抑制方法。 The scale suppression method according to any one of claims 1 to 3, wherein a pH of the geothermal water is adjusted to 9 or more. 　前記地熱水に、前記スケール抑制剤の添加と同時又は前記スケール抑制剤の添加後に、アルカリ剤を添加してｐＨを９以上に調整する請求項４に記載のスケール抑制方法。 The scale suppression method according to claim 4, wherein the pH is adjusted to 9 or more by adding an alkaline agent to the geothermal water simultaneously with the addition of the scale inhibitor or after the addition of the scale inhibitor. 　前記熱除去工程は、前記地熱水を減圧し、水蒸気を取出すフラッシュ工程及び／又は前記地熱水から熱を回収して発電媒体を蒸発させる工程を含む請求項１に記載のスケール抑制方法。 2. The scale suppression method according to claim 1, wherein the heat removal step includes a flash step of decompressing the geothermal water and taking out water vapor and / or a step of recovering heat from the geothermal water and evaporating the power generation medium. 　前記生産井から採取した地熱水を気液分離し、気液分離後の蒸気を発電設備に供給し、気液分離後の地熱水を前記熱除去工程に送る、請求項１に記載のスケール抑制方法。 The geothermal water collected from the production well is gas-liquid separated, the vapor after gas-liquid separation is supplied to a power generation facility, and the geothermal water after gas-liquid separation is sent to the heat removal step. Scale suppression method. 　生産井から採取される地熱水中の２価以上の無機陽イオン濃度を測定する無機陽イオン濃度測定装置と、
　前記生産井から採取される地熱水の流量を測定する流量計と、
　前記地熱水の温度を低下させる熱除去部と、
　前記熱除去後の地熱水の温度を測定する温度計と、
　前記熱除去後の地熱水のｐＨを計測するｐＨ測定装置と、
　前記熱除去部で温度を低下させた後の地熱水の温度及びｐＨに基づいて、前記熱除去部で温度を低下させた後の地熱水の無機陽イオンの飽和濃度を求め、前記無機陽イオン濃度測定装置で測定した前記地熱水の無機陽イオン濃度から前記熱除去部で温度を低下させた後の地熱水の無機陽イオンの飽和濃度を引いた値と、前記地熱水の流量とから、前記無機陽イオンを含む塩の析出を抑制するために必要なスケール抑制剤の添加量を算出する演算処理部と、
　前記地熱水に、前記演算処理部で算出された量のスケール抑制剤を添加する制御部とを備えていることを特徴とする地熱発電装置。 An inorganic cation concentration measuring device that measures the concentration of divalent or higher inorganic cations in geothermal water collected from production wells;
A flow meter for measuring the flow rate of geothermal water collected from the production well;
A heat removal section for lowering the temperature of the geothermal water;
A thermometer for measuring the temperature of the geothermal water after the heat removal;
A pH measuring device for measuring the pH of the geothermal water after the heat removal;
Based on the temperature and pH of the geothermal water after the temperature is lowered at the heat removal unit, the saturation concentration of the inorganic cation of the geothermal water after the temperature is lowered at the heat removal unit is determined, and the inorganic A value obtained by subtracting the saturation concentration of the inorganic cation of the geothermal water after the temperature has been lowered by the heat removal unit from the inorganic cation concentration of the geothermal water measured by a cation concentration measuring device, and the geothermal water From the flow rate of, the arithmetic processing unit that calculates the amount of scale inhibitor added to suppress precipitation of the salt containing the inorganic cation,
A geothermal power generation apparatus comprising: a controller that adds an amount of the scale inhibitor calculated by the arithmetic processing unit to the geothermal water. 　前記熱除去部の前段に、気液分離器が配置され、気液分離後の地熱水を前記熱除去部に導入するように構成されている、請求項８に記載の地熱発電装置。 The geothermal power generator according to claim 8, wherein a gas-liquid separator is disposed in front of the heat removal unit, and geothermal water after gas-liquid separation is introduced into the heat removal unit. 　前記熱除去部は、放熱する配管、減圧により地熱水から蒸気を取出すフラッシャー及び発電媒体に熱を与えて発電媒体を蒸発させる熱交換器、から選ばれる１種以上である請求項８に記載の地熱発電装置。 The said heat removal part is 1 or more types chosen from the heat exchanger which heat-dissipates heat generation piping, the flasher which extracts vapor | steam from geothermal water by decompression, and heat-generates a power generation medium, and heat-generation medium. Geothermal power generator. 　試料水を貯留する溶液貯留部と、
　この溶液貯留部に貯留された試料水の温度を調整する温度制御部と、
　前記溶液貯留部に貯留された試料水に酸又はアルカリを添加して、ｐＨを調整するｐＨ調整部と、
　所定時間経過後に試料水中の２価以上の無機陽イオン濃度を測定する濃度計測部と、
　試料水として前記無機陽イオン濃度を徐々に高めたものを作成して順次、前記溶液貯留部に流入させる溶液供給部とを有する無機陽イオンの飽和濃度測定装置を備えている請求項８～１０のいずれか１つに記載の地熱発電装置。 A solution reservoir for storing sample water;
A temperature control unit for adjusting the temperature of the sample water stored in the solution storage unit;
A pH adjusting unit for adjusting pH by adding acid or alkali to the sample water stored in the solution storing unit;
A concentration measuring unit for measuring a divalent or higher inorganic cation concentration in the sample water after elapse of a predetermined time;
An inorganic cation saturation concentration measuring device comprising a solution supply unit for preparing sample water having a gradually increased concentration of the inorganic cation and sequentially flowing the sample water into the solution storage unit. A geothermal power generation apparatus according to any one of the above.
PCT/JP2012/055545 2011-04-19 2012-03-05 Scale inhibition method and geothermal power generating device Ceased WO2012144277A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US14/009,296 US9840429B2 (en) 2011-04-19 2012-03-05 Scale inhibition method and geothermal power generating device
PH1/2013/502042A PH12013502042B1 (en) 2011-04-19 2012-03-05 Scale inhibition method and geothermal power generating device
NZ615602A NZ615602B2 (en) 2011-04-19 2012-03-05 Scale inhibition method and geothermal power generating device
JP2013510917A JP5839030B2 (en) 2011-04-19 2012-03-05 Scale suppression method and geothermal power generator

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2011-092758 2011-04-19
JP2011092758 2011-04-19

Publications (1)

Publication Number Publication Date
WO2012144277A1 true WO2012144277A1 (en) 2012-10-26

Family

ID=47041399

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2012/055545 Ceased WO2012144277A1 (en) 2011-04-19 2012-03-05 Scale inhibition method and geothermal power generating device

Country Status (4)

Country Link
US (1) US9840429B2 (en)
JP (1) JP5839030B2 (en)
PH (1) PH12013502042B1 (en)
WO (1) WO2012144277A1 (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2722599A1 (en) * 2012-10-16 2014-04-23 Panasonic Corporation Water heater
EP2722598A1 (en) * 2012-10-16 2014-04-23 Panasonic Corporation Water heater
WO2015181999A1 (en) * 2014-05-26 2015-12-03 三菱重工業株式会社 Water treatment device and water treatment method
JP2016142451A (en) * 2015-02-02 2016-08-08 イノベーティブ・デザイン＆テクノロジー株式会社 Heat exchanger for power generation system, binary power generation system including the heat exchanger, and control method for heat exchanger for power generation system
US9657600B2 (en) 2015-02-02 2017-05-23 Innovative Designs & Technology Inc. Heat exchanger, a purifier, an electrode-containing pipe, a power generation system, a control method for heat exchanger and a scale removing method
JP2017198142A (en) * 2016-04-27 2017-11-02 株式会社Ｉｈｉ回転機械 Binary power generation system and binary power generation method
JP2018030088A (en) * 2016-08-24 2018-03-01 株式会社日本触媒 Scale inhibitor for geothermal power generation devices, and scale prevention method for geothermal water
JPWO2016204287A1 (en) * 2015-06-19 2018-04-05 ジャパン・ニュー・エナジー株式会社 Geothermal power generation system, geothermal power generation apparatus, geothermal power generation method or medium transfer pipe, geothermal power generation apparatus and geothermal power generation method using the medium transfer pipe, and method of installing a medium transfer pipe in a crushing zone
JP2018091809A (en) * 2016-12-07 2018-06-14 三菱日立パワーシステムズ株式会社 Device, system, and method for vapor characteristic monitoring for geothermal power generation, and geothermal power generation system control method
JP2020012456A (en) * 2018-07-20 2020-01-23 株式会社東芝 Scale suppression device, geothermal power generation facility and scale suppression method
JP7094047B1 (en) 2021-02-24 2022-07-01 日本重化学工業株式会社 Geothermal turbine blade scale removal method and geothermal power generation method
JP2022177574A (en) * 2021-05-18 2022-12-01 富士電機株式会社 Scrubber device
JP2023513422A (en) * 2020-01-21 2023-03-31 ソレニス・テクノロジーズ・ケイマン・エル・ピー Stimulation of geothermal wells and removal of silica deposits
JPWO2023074697A1 (en) * 2021-10-25 2023-05-04
WO2024057966A1 (en) * 2022-09-12 2024-03-21 富士電機株式会社 pH ESTIMATION DEVICE AND pH ESTIMATION METHOD FOR SILICA-OVERSATURATED FLUID
WO2025018200A1 (en) * 2023-07-19 2025-01-23 富士電機株式会社 Geothermal power generation system
WO2025018198A1 (en) * 2023-07-19 2025-01-23 富士電機株式会社 Geothermal power generation system

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7438970B2 (en) * 2018-04-18 2024-02-27 エコラボ ユーエスエー インコーポレイティド Turbine deposit cleaner
US11230484B2 (en) * 2018-09-12 2022-01-25 Chemtreat, Inc. Methods and systems for calcite removal using polysuccinimide
US11421516B2 (en) 2019-04-30 2022-08-23 Sigl-G, Llc Geothermal power generation
US11897801B2 (en) * 2019-07-30 2024-02-13 Solenis Technologies, L.P. Silica scale inhibitors
WO2022051019A1 (en) * 2020-09-04 2022-03-10 Chemtreat, Inc. Methods for predicting and monitoring scale formation in industrial water systems
JP7145375B2 (en) * 2021-01-29 2022-10-03 栗田工業株式会社 Estimation device, prediction device, control device, estimation system, prediction system, control system, estimation program, prediction program, control program, estimation method, prediction method, and control method
CN114412416B (en) * 2022-03-09 2025-06-27 山东省鲁南地质工程勘察院(山东省地质矿产勘查开发局第二地质大队) A geothermal heat reservoir and transmission pipeline non-pump descaling device and use method
JP7182027B1 (en) * 2022-08-05 2022-12-01 カルファケミカル株式会社 Binary power generation system using renewable energy such as geothermal heat

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57112697A (en) * 1980-12-29 1982-07-13 Mitsubishi Metal Corp Method of removing scale on surface of heat-exchange tube
JPS61220793A (en) * 1985-03-25 1986-10-01 Sasakura Eng Co Ltd Method for monitoring and controlling water quality
JPS6274499A (en) * 1985-09-27 1987-04-06 Hisaka Works Ltd How to remove scale from hot spring water
JPS62111095A (en) * 1985-11-09 1987-05-22 株式会社ササクラ Dual-purpose treatment method of geothermal water
JPH0448998A (en) * 1990-06-19 1992-02-18 Hitachi Zosen Corp Method for suppressing scale precipitation in geothermal utilization equipment
JPH04281899A (en) * 1991-03-11 1992-10-07 Hitachi Zosen Corp Method for suppressing scale precipitation in geothermal utilization equipment
JPH09206733A (en) * 1995-08-25 1997-08-12 Union Oil Co Calif Method of preventing the formation of silicon-containing precipitates

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2769461B2 (en) 1992-01-17 1998-06-25 日本重化学工業株式会社 Geothermal steam well chemical tube mounting structure
JP3244855B2 (en) 1993-04-21 2002-01-07 三菱重工業株式会社 Prevention of silica scale precipitation from geothermal hot water
US5656172A (en) * 1995-12-28 1997-08-12 Union Oil Company Of California pH modification of geothermal brine with sulfur-containing acid
JP2002250271A (en) * 2001-02-23 2002-09-06 Toshiba Eng Co Ltd Scale deposition monitoring system of geothermal power generation steam turbine
JP2002257030A (en) * 2001-02-28 2002-09-11 Mitsubishi Materials Corp Scale growth prediction device, method, program thereof, and recording medium recording program
US6761865B1 (en) * 2003-04-22 2004-07-13 Union Oil Company Of California Method for synthesizing crystalline magnesium silicates from geothermal brine
US8563481B2 (en) * 2005-02-25 2013-10-22 Clearwater International Llc Corrosion inhibitor systems for low, moderate and high temperature fluids and methods for making and using same
JP5125970B2 (en) * 2008-10-07 2013-01-23 富士電機株式会社 Scale adhesion monitoring device for geothermal fluid utilization system
US8430162B2 (en) * 2009-05-29 2013-04-30 Schlumberger Technology Corporation Continuous downhole scale monitoring and inhibition system
JP5372838B2 (en) * 2010-05-31 2013-12-18 富士電機株式会社 Scale suppression device

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57112697A (en) * 1980-12-29 1982-07-13 Mitsubishi Metal Corp Method of removing scale on surface of heat-exchange tube
JPS61220793A (en) * 1985-03-25 1986-10-01 Sasakura Eng Co Ltd Method for monitoring and controlling water quality
JPS6274499A (en) * 1985-09-27 1987-04-06 Hisaka Works Ltd How to remove scale from hot spring water
JPS62111095A (en) * 1985-11-09 1987-05-22 株式会社ササクラ Dual-purpose treatment method of geothermal water
JPH0448998A (en) * 1990-06-19 1992-02-18 Hitachi Zosen Corp Method for suppressing scale precipitation in geothermal utilization equipment
JPH04281899A (en) * 1991-03-11 1992-10-07 Hitachi Zosen Corp Method for suppressing scale precipitation in geothermal utilization equipment
JPH09206733A (en) * 1995-08-25 1997-08-12 Union Oil Co Calif Method of preventing the formation of silicon-containing precipitates

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2722598A1 (en) * 2012-10-16 2014-04-23 Panasonic Corporation Water heater
EP2722599A1 (en) * 2012-10-16 2014-04-23 Panasonic Corporation Water heater
WO2015181999A1 (en) * 2014-05-26 2015-12-03 三菱重工業株式会社 Water treatment device and water treatment method
JP2015223539A (en) * 2014-05-26 2015-12-14 三菱重工業株式会社 Water treatment equipment and water treatment method
JP2016142451A (en) * 2015-02-02 2016-08-08 イノベーティブ・デザイン＆テクノロジー株式会社 Heat exchanger for power generation system, binary power generation system including the heat exchanger, and control method for heat exchanger for power generation system
US9657600B2 (en) 2015-02-02 2017-05-23 Innovative Designs & Technology Inc. Heat exchanger, a purifier, an electrode-containing pipe, a power generation system, a control method for heat exchanger and a scale removing method
JPWO2016204287A1 (en) * 2015-06-19 2018-04-05 ジャパン・ニュー・エナジー株式会社 Geothermal power generation system, geothermal power generation apparatus, geothermal power generation method or medium transfer pipe, geothermal power generation apparatus and geothermal power generation method using the medium transfer pipe, and method of installing a medium transfer pipe in a crushing zone
JP2017198142A (en) * 2016-04-27 2017-11-02 株式会社Ｉｈｉ回転機械 Binary power generation system and binary power generation method
JP2018030088A (en) * 2016-08-24 2018-03-01 株式会社日本触媒 Scale inhibitor for geothermal power generation devices, and scale prevention method for geothermal water
JP2018091809A (en) * 2016-12-07 2018-06-14 三菱日立パワーシステムズ株式会社 Device, system, and method for vapor characteristic monitoring for geothermal power generation, and geothermal power generation system control method
JP2020012456A (en) * 2018-07-20 2020-01-23 株式会社東芝 Scale suppression device, geothermal power generation facility and scale suppression method
JP7077169B2 (en) 2018-07-20 2022-05-30 株式会社東芝 Scale suppression device, geothermal power generation equipment and scale suppression method
JP2023513422A (en) * 2020-01-21 2023-03-31 ソレニス・テクノロジーズ・ケイマン・エル・ピー Stimulation of geothermal wells and removal of silica deposits
US12371972B2 (en) 2020-01-21 2025-07-29 Solenis Technologies, L.P. Geothermal well stimulation and silca based deposit removal
JP7094047B1 (en) 2021-02-24 2022-07-01 日本重化学工業株式会社 Geothermal turbine blade scale removal method and geothermal power generation method
JP2022129307A (en) * 2021-02-24 2022-09-05 日本重化学工業株式会社 Geothermal turbine blade descaling method and geothermal power generation method
WO2022181679A1 (en) * 2021-02-24 2022-09-01 日本重化学工業株式会社 Method for removing scale from geothermal turbine blade and method for geothermal power generation
JP2022177574A (en) * 2021-05-18 2022-12-01 富士電機株式会社 Scrubber device
JP7661782B2 (en) 2021-05-18 2025-04-15 富士電機株式会社 Scrubber Equipment
JPWO2023074697A1 (en) * 2021-10-25 2023-05-04
WO2023074697A1 (en) * 2021-10-25 2023-05-04 富士電機株式会社 Method for predicting generated amount of silica scale
JP7681263B2 (en) 2021-10-25 2025-05-22 富士電機株式会社 Method for predicting the amount of silica scale formation
WO2024057966A1 (en) * 2022-09-12 2024-03-21 富士電機株式会社 pH ESTIMATION DEVICE AND pH ESTIMATION METHOD FOR SILICA-OVERSATURATED FLUID
JPWO2024057966A1 (en) * 2022-09-12 2024-03-21
JP7769925B2 (en) 2022-09-12 2025-11-14 富士電機株式会社 pH estimation device and pH estimation method for silica-supersaturated fluid
WO2025018200A1 (en) * 2023-07-19 2025-01-23 富士電機株式会社 Geothermal power generation system
WO2025018198A1 (en) * 2023-07-19 2025-01-23 富士電機株式会社 Geothermal power generation system

Also Published As

Publication number Publication date
US20140083949A1 (en) 2014-03-27
PH12013502042A1 (en) 2013-12-16
JPWO2012144277A1 (en) 2014-07-28
NZ615602A (en) 2015-02-27
JP5839030B2 (en) 2016-01-06
PH12013502042B1 (en) 2017-11-17
US9840429B2 (en) 2017-12-12

Similar Documents

Publication Publication Date Title
JP5839030B2 (en) Scale suppression method and geothermal power generator
JP5751987B2 (en) Scale suppression method and geothermal power generator
van Wyk et al. Analysis of the energy consumption of supercritical water desalination (SCWD)
CN101614502B (en) A cleaning method for a low-temperature multi-effect seawater desalination evaporator
von Hirtz Silica scale control in geothermal plants—Historical perspective and current technology
JP2014036912A (en) Method for preventing silica scale in water system and scale inhibitor, and water treatment method and water treatment agent for preventing silica scale and corrosion of metals
JP5563854B2 (en) Scale suppression method and power generation system
Luo et al. Scaling tendency of boiler feedwater without desiliconization treatment
BR112015025008B1 (en) METHOD FOR REMOVING SCALES IN STEAM GENERATION INSTALLATION
JP6056183B2 (en) Scale suppression device, geothermal power generation system using the device, and scale suppression method
JP6592386B2 (en) Method and apparatus for treating ammonia-containing wastewater
Jiang et al. Proof-of-concept study of an integrated solar desalination system
JP5906926B2 (en) Scale suppression device, geothermal power generation system using the device, and scale suppression method
JP5953882B2 (en) Water quality control method for circulating cooling water
Rahman et al. 14 Scale Formation and Control in Thermal Desalination Systems
JP2016031154A (en) Control method, boiler control device, and program
Myers et al. Purification of magnesium chloride from mixed brines via hydrogen chloride absorption with ambient temperature and pressure regeneration of super azeotropic hydrochloric acid
NZ615602B2 (en) Scale inhibition method and geothermal power generating device
US20240426283A1 (en) Geothermal power generation system and silica scale deposition control method
JP2018153732A (en) Reverse osmosis treatment method and device
Mabrouk et al. Modelling scale formation in wet cooling system and validation with pilot plant data
JP2012107819A (en) Steam boiler apparatus
JP2020133992A (en) Ground source heat utilization system
Inyang et al. The importance of boiler feed water and its treatment in a chemical plant
Anadebe et al. Scales, Scaling, and Antiscalants: Fundamentals, Mechanisms, and Properties

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12773822

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2013510917

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 14009296

Country of ref document: US

122 Ep: pct application non-entry in european phase

Ref document number: 12773822

Country of ref document: EP

Kind code of ref document: A1